HIGH-VISCOUS LUBRICANT COPOLYMER COMPATIBLE WITH NON-POLAR BASE FLUIDS

Abstract: The invention pertains to a lubricant or lubricant additive having a viscosity ranging from 200 to 1100 cSt which at the same time is compatible with non-polar base fluids such as poly( alpha -olefins), and which comprises a copolymer of an alpha -olefin having of from 8 to 18 carbon atoms and a fumaric diester having an aliphatic alcohol as the esterifying component, the copolymer having a weight average molecular weight above approximately 3500, and the esterifying component being C8 to C10 alcohol (linear or branched) or iso-C13 alcohol. Also disclosed is a process for the preparation of the copolymers wherein an alpha -olefin having of from 8 to 18 carbon atoms is reacted with a fumaric diester under the influence of a peroxide radical initiator having tertiary alkyl groups while applying a temperature of from 110 DEG C to 150 DEG C.

Description: HIGH-VISCOUS LUBRICANT COPOLYMER COMPATIBLE WITH NON-POLAR BASE FLUIDS The invention pertains to a copolymer suitable for use in or as a lubricant, which copolymer is made up of an α-olefin and a (di)ester of an ,β ethylenically unsaturated dicarboxylic acid. More particularly, the invention pertains to a lubricant or lubricant additive comprising a copolymer of an α-olefin having of from 8 to 18 carbon atoms and a fumaric diester having an aliphatic alcohol as the esterifying component. Copolymers of this class are known, particularly in the field of lubricants. Thus, copolymers as indicated above are disclosed in US 2,543,964 (Giammaria) as pour-point depressing additives for lubricating mineral oils. Giammaria employs α-olefins having of from 8 to 18 carbon atoms and aleic or fumaric di esters of alcohols having 12 or more carbon atoms. Disclosed in particular are copolymers of Cβ α-olefin and C Q α-olefin with fumaric diesters of C12 alcohol, C14 alcohol, and the Lorol-B ® mixture of C^Q to ^18 alcohols which has C12 and C14 alcohols as the main constituents. In US 2,666,746 (Munday) the production is disclosed of copolymers of a fumaric acid ester of Cβ_i8 alcohol, particularly decyl , lauryl, or tetradecyl alcohol, and a vinyl ester of a fatty acid. Copolymers within the above class are also disclosed in EP 75217. The esters are preferably diesters of maleic or fumaric acid, the esterifying alcohols being linear and branched alcohols having of from 3 to 10 carbon atoms. The α-olefins employed have of from 10 to 16 carbon atoms. The disclosed copolymers are suitable as lubricants and lubricant additives, and characteristically have low pour-points, molecular weights of from 1300 to 3250, and viscosities at 100°C of maximally about 80 cSt. JP 157687/1980 generically discloses copolymers of the above type, employing maleic and fumaric esters of alcohols with chain lengths varied within the range of Cj to Q, preferably Ci to Cg, and α- olefins having of from 4 to 60 carbon atoms. Also Grava, US 4,526,950, provides a disclosure of a general nature regarding the above type of copolymers. Described are interpolymers of α-olefins having at least about 6 carbon atoms and unsaturated carboxylic acids or derivatives thereof. Acids mentioned are maleic and fumaric acid. As an acid derivative maleic anhydride, which is the comonomer of preferred choice, is specifically referred to. US 2,615,845 to Lippincott discloses lubricating o ' il additives which may be copolymers of α-olefins having of from 2 to 18 carbon atoms and .β ethylenically unsaturated carboxylic acids and their derivatives, notably anhydrides (e.g., maleic anhydride). The copolymers may be modified, e.g., by esterification. Suitable esterifying alcohols are said to range from ethanol to octadecanol . In particular, Lippincott teaches esterification with the above-mentioned mixture Lorol-B® Kagan, in US 3,314,908, discloses specific copolymers of a 04.9 α- olefin and fumaric diesters wherein two different esterifying alcohols are present either as mixed esters or as a mixture of single alcohol diesters, one alcohol having a chain length of C _3 and the other of 0 .9. The Kagan copolymers are tough, flexible solids which serve as a paint vehicle. In EP 296714 lubricating oil flow improvers are disclosed which may be copolymers of unsaturated dicarboxy esters with, e.g., α-olefins. In the case of α-olefins being used, maleic anhydride is explicitly preferred as the dicarboxylic monomer. It is also disclosed to esterify the carboxyl groups, either before or after copolymerization, with Ci to C20 alcohols. Preferred are Cg to Z\Q aliphatic alcohols. Suitable α-ofefins are said to contain between about 6 and 46 carbon atoms. In EP 365 081 a two-cycle engine oil composition is disclosed in which a copolymer of the above category is employed. Preferred α-olefins have of from 6 to 18 carbon atoms. These are typically copolymerized with esters of maleic, fumaric, or other a,β ethylenically unsaturated dicarboxylic acids, the esterifying alcohols having 1 to 20 carbon atoms. Preferred are C3 to Cg alcohols. In EP 429 123 compositions from α,ø-unsaturated dicarboxylic acid esters and olefinically unsaturated compounds are disclosed. The compositions are suitable for use as lubricants and lubricant additives and comprise a substantial amount of an intermediate molecular weight reaction product which is neither the lower molecular weight alkenyl or alkyl succinic reaction product, nor the copolymer of the olefin and the ester. While the prior art thus comprises viable lubricants and lubricant additives, the disclosed copolymers fall short when it comes to satisfying the demands that are the object of the present invention. There is a need to provide lubricants and lubricant additives that are compatible with non-polar base fluids like poly α-olefins (PAO), hydrocracked basestocks, polyisobutylenes, and the like. At the same time, these lubricants should have a high viscosity and be able to boost the viscosity of the non-polar base fluids in conjunction with which they can be used as an additive, and/or act as a viscosity index improver therefor. For known copolymers of the above-identified class, these demands appear incompatible. These demands are now satisfied by virtue of the present invention. To this end the invention provides lubricants and lubricant additives comprising a copolymer within the general class indicated in the opening paragraph, on the basis of α-olefins having of from 8 to 18 carbon atoms and a fumaric diester having an aliphatic alcohol as the esterifying component, the copolymer having a weight average molecular weight above approximately 3500, and wherein the esterifying component is selected from the group consisting of linear octanol , branched octanol , linear nonanol , branched nonanol , linear decanol , branched decanol , branched tridecanol, and mixtures thereof. These copolymers, which form a novel selection within the general class outlined above, display desirable properties, including a viscosity at 100°C of more than 200 mm 2 /sec (cSt) and good PAO compatibility. Furthermore, they are liquid at room temperature and despite their relatively high viscosities have relatively low pour- points. Other advantages include a high viscosity index and a good load carrying capacity. Furthermore, the average molecular weights, though above approximately 3500, are relatively low in respect of the high viscosities. This makes the copolymers shear stable. The copolymers can suitably be used as multi-purpose additives to engine oils: they can be used as a shear-stable viscosity index improver, but also as an anti-wear additive. The instant copolymers are particularly useful as an adjuvant for synthetic gear oils. A description of various embodiments of the invention is given below. The α-olefins may be selected from linear or branched α-olefins having of from 8 to 18 carbon atoms. Shorter α-olefins are not very suitable due to their low boiling point, longer α-olefins generally yield copolymers that are not sufficiently compatible with non-polar base fluids such as PAO. Suitable examples of α-olefins are 1-octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, 1-octadecene. Mixtures of linear and/or branched α-olefins can also be employed. Further, it should be noted that commercially available olefins are generally mixtures characterized by a predominant olefin species and a predominant or average carbon number content. Such commercially available mixtures comprising in substantial part α-olefins with minor amounts of internal olefins and vinylidene compounds are particularly preferred, as they will lead to copolymers having the highest viscosities. Preferred are the C 2 t0 ^16 α-olefins, with the C14 to Cj α-olefins being most preferred. It is a requirement that the a,β ethylenically unsaturated dicarboxylic diester selected be a fumaric ester. This is a deviation from the trend in the art, where either maleic and fumaric diesters are recognized as being equally viable, or maleic acid is preferred. A quintessential aspect of the present invention is the selection of the appropriate esterifying alcohol component. E.g., it was found that the Lorol-B® mixture employed in the prior art yielded unsatisfactory results. Notably, the resulting copolymers are not PAO compatible. It was established, in accordance with the present invention, that the desired combination of thus far incompatible properties can be achieved by employing as the esterifying component an alcohol having of from 8 to 10 carbon atoms. It was further established that, while esterifying alcohols having more than 10 carbon atoms do not yield copolymers possessing the required compatibility with non-polar base fluids, unexpectedly a highly suitable copolymer in this respect is formed if iso-Ci3 alcohol is employed. It is also possible to employ mixtures of alcohols, preferably all selected from the group consisting of linear octanol, branched octanol, linear nonanol, branched nonanol, linear decanol, branched decanol, and branched tridecanol. It should be noted that the nature of the present copolymers will not be drastically changed by minor additions of other alcohols, nor by minor additions of α-olefins outside the above scope or the use of minor amounts of an a,β ethylenically unsaturated dicarboxylic ester other than a difumarate. It should be noted, though, that an increased acid number has a negative effect on the product's stability, which particularly is a drawback for use in gear-oils. Hence, in gear-oils the amount of monoesters (monofumarates) present should be kept as low as possible, and preferably monoesters are avoided altogether. The monomer ratio of α-olefin to difumarate is generally within the range of from about 4:1 to about 1:2, and preferably of from about 2:1 to about 1:1. It is a further requirement that the copolymer have a weight average molecular weight above approximately 3500. For example, it is for that reason among others that the copolymers disclosed in EP 75217 are unsuitable for meeting the demands underlying the present invention. The man skilled in the art of copolymerization generally knows how to vary reaction conditions so as to achieve the required molecular weight. However, the invention also pertains to a method which was found to be particularly suitable for preparing the copolymers having the unexpected and desirable combination of properties outlined hereinbefore. The method of the invention comprises reacting the α-olefin and the fumaric diester under the following conditions: applying a polymerization temperature below approximately 160°C, preferably within the range of from 110°C to 150°C, and optimally between 120°C and 140°C; employing a radical initiator, such as a peroxide, displaying favourable decomposition in the above temperature range; dosing the initiator continuously to a reaction mixture of the α- olefin and the difumarate. If needed, PAO compatibility can be improved by dosing both the initiator and the difumarate to the α- olefin; It should be noted that a process for the preparation of a copolymer of an α-olefin and a fumaric diester wherein an α-olefin having of from 8 to 18 carbon atoms is reacted with a fumaric diester under the influence of a peroxide radical initiator while applying elevated temperature, is known from the aforementioned Giammaria disclosure, • c Giammaria generally employs lower temperatures than is the case with the preferred process of the invention, and the resulting products were found to lack PAO compatibility. As indicated above, the copolymers of the present invention are 1Q suitable as lubricants. That is, they possess sufficient lubricating properties for use as a lubricant base fluid. As base fluids they are particularly suitable for use in high-temperature applications in the industrial lubricant market. 5 More importantly, however, the copolymers of the invention provide lubricant additives that are compatible with non-polar base fluids such as poly α-olefins (PAO), e.g., PAO-6, PAO-8, and PAO-10, which are particularly used in 4-stroke engine oils and gear-oils, hydrocracked basestocks, which are also used in 4-stroke engine oils, 0 and polyisobutylenes and the like (used in 2-stroke engine oils), and at the same time have a sufficiently high viscosity. They are compatible with these non-polar base fluids over a wide temperature range: even at temperatures as low as -25°C the copolymers are PAO-compatible at substantially every weight ratio (the lower the 5 temperature, the more compatibility problems are normally to be expected). The high viscosity is advantageous in that the viscosity of the non-polar base stocks can be boosted without adversely affecting the low temperature viscosimetrics. In this respect it is preferred that the copolymers have a low pour-point. 0 The copolymers of the present invention have viscosities at 100°C of more than at least 200 mm 2 /sec and in preferred cases of 300 mm 2 /sec or higher, e.g., up to about 1100 mm 2 /sec. Preferred copolymers in thi s respect empl oy branched al cohol s as the esteri fyi ng component . Sti l l more preferred copolymers, whi ch combi ne a high vi scosity with a l ow pour-point, employ i so-Cβ al cohol . The preferred copolymers di spl ay the combi ned properties of havi ng a high vi scosity, a high vi scosity index, and a low pour poi nt. Further, the copolymers of the present invention are able to enhance the viscosity of the non-polar base fluids in conjunction with which they can be used as an additive and may also improve (enhance) the viscosity index thereof. A high viscosity index is important, as for many applications, notably engine lubricants, the lubricant's flow properties should not substantially change as a result of temperature changes. The invention will be further illustrated with reference to the following unlimitative examples. EXAMPLE 1 In a reaction vessel 168 g C12 α-olefin and 340 g di-isooctyl fumarate (difumarate of 2-ethylhexyl alcohol) were heated, with stirring, to 120°C. While the temperature was kept at this level, 1.5 ml t-butyl peroxy-3,5,5-trimethylhexanoate were dosed continuously, with stirring, over a period of 3 hours. After one further hour of stirring at 120°C, volatiles (94 g) were removed in vacuo. The product subsequently obtained was a colourless, viscous liquid copolymer of the α-olefin and the difumarate. Characteristic properties of the product are a pour-point (measured in accordance with ASTM D 97) of -15°C, a viscosity at 100°C (measured in accordance with ASTM D 445) of 796 mm 2 /sec, a weight average molecular weight (determined by size exclusion chromatography = SEC) of 6800, and a viscosity index (determined in accordance with ASTM D 2270) of 254. An amount of 10% by weight of the copolymer was added to PAO-6 (i.e., a poly(α-olefine having a viscosity at 100°C of 6 cSt (mm 2 /sec) . At -25°C a clear solution was obtained. EXAMPLE 2 Following an essentially similar procedure to that outlined in Example 1, the copolymers in accordance with the invention listed in Table 1 were prepared. Isooctanoldifumarate means the diester of fumaric acid and 2-ethylhexyl alcohol. Isotridecanoldifumarate means the diester of fumaricester and a commercially available mixture of primary isotridecanoles (generally prepared by Oxo-synthesis from tetrapropylene) . All copolymers in accordance with the invention displayed good PAO compatibility in that at 4°C a clear solution of 10% by weight in PAO-6 was obtained. TABLE 1 (All readily-compatible with PA0-6) α-Olefin Difumarate Mol .wt. Vise. VI Pour-Point mm 2 /s °C 1-octene iso-octanol 735 239 - 5°C 1-octene n-decanol 9100 233 232 -26°C 1-decene iso-octanol 7400 1098 263 -10°C 1-dodecene iso-decanol 7200 641 226 -14°C 1-tetradecene iso-octanol 6700 668 251 -18°C 1-tetradecene iso-decanol 7050 600 227 -15°C 1-hexadecene n-octanol 9100 302 250 -29°C 1-hexadecene iso-octanol 6600 486 242 -23°C 1-hexadecene n-decanol 8400 250 245 -23°C 1-hexadecene iso-decanol 8050 636 236 - 7°C 1-octadecene iso-octanol 7000 427 237 -18°C EXAMPLE 3 Following an essentially similar procedure to that outlined in Example 1, copolymers were prepared employing iso-tridecanoldifumarate. These copolymers displayed a good PAO compatibility in that at 4°C a clear solution of 10% by weight in PAO-6 was obtained. The copolymer of 1-octene and iso-tridecanoldifumarate had a molecular weight of 6400, displayed a viscosity of 542 mm 2 /sec, and had a viscosity index of 199. The copolymer of 1-hexadecene and iso-tridecanoldifumarate had a mol-ecular weight of 7400, a viscosity of 534 mm 2 /sec, and a viscosity index of 221. Of the latter copolymer also the pour point was measured: -15°C. COMPARATIVE EXAMPLE 1 Following an essentially similar procedure to that outlined in Example 1, the copolymers ncrt in accordance with the invention listed in Table 2 were prepared. All copolymers jτot in accordance with the invention displayed poor PAO compatibility in that at 4°C solution of 10% by weight in PAO-6 turned out to be hazy. TABLE 2 (All poor!y compatible with PAO-6) α-Olefin Difumarate Mol.wt. Vise. VI Pour-Point mm 2 /s °C 1-octene n-hexanol 380 231 -19°C 1-octene n-dodecanol 8600 180 226 - 7°C 1-dodecene iso-butanol 7050 2902 +20°C 1-dodecene n-hexanol 7100 371 239 -22°C 1-dodecene 1-dodecanol 8800 237 274 - 5°C 1-tetradecene n-butanol 8100 652 . 235 -18°C 1-tetradecene iso-butanol 7700 2300 +20°C 1-hexadecene n-butanol 8100 469 230 -19°C 1-hexadecene iso-butanol 7150 1200 181 +11°C 1-hexadecene n-dodecanol 9000 238 245 + 4°C 1-eicosene iso-octanol 7500 228 202 +30°C 1-eicosene iso-decanol 7400 289 +20°C 1-eicosene iso-tridecanol 5600 210 +22°C

Claims: CLAIMS 1. A lubricant or lubricant additive comprising a copolymer of an α- olefin having of from 8 to 18 carbon atoms and a fumaric diester having an aliphatic alcohol as the esterifying component, characterized in that the copolymer has a weight average molecular weight above approximately 3500, and wherein the esterifying component is selected from the group consisting of linear octanol, branched octanol, linear nonanol, branched nonanol, linear decanol, branched decanol, branched tridecanol, and mixtures thereof. 2. A lubricant or lubricant additive comprising a copolymer of an α- olefin having of from 8 to 18 carbon atoms and a fumaric diester having an aliphatic alcohol as the esterifying component, characterized in that the copolymer has a weight average molecular weight above approximately 3500, and wherein the esterifying component is a Cg to C Q alcohol. 3. A lubricant or lubricant additive comprising a copolymer of an α- olefin having of from 8 to 18 carbon atoms and a fumaric diester having an aliphatic alcohol as the esterifying component, characterized in that the copolymer has a weight average molecular weight above approximately 3500, and wherein the esterifying component is iso-Ci3 alcohol. 4. A lubricant or lubricant additive according to any one of the preceding claims, characterized in that the α-olefin has 12 to 16 carbon atoms. 5. A lubricant or lubricant additive according to claim 4, characterized in that the esterifying component is iso-C^o alcohol . 6. A lubricant or lubricant additive according to claim 4, characterized in that the esterifying component is iso-C8 alcohol. 7. A lubricating oil composition comprising poly(α-olefine) and an amount of 1 to 70 wt%, preferably 5 to 50 wt%, of an additive in accordance with any one of the preceding claims. 8. A process for the preparation of a copolymer of an α-olefin and a fumaric diester wherein an α-olefin having of from 8 to 18 carbon atoms is reacted with a fumaric diester under the influence of a peroxide radical initiator while applying elevated temperature, characterized in that the temperature is kept within the range of from 110°C to 150°C. 9. A process according to claim 8, characterized in that the peroxide i s t-butyl peroxy-3 , 5 , 5-trimethyl hexanoate . 10. A copolymer obtainable by a process according to claim 9 or 10. 11. A copolymer of an α-olefin and a fumaric diester having an aliphatic alcohol as the esterifying component, characterized in that the copolymer has a weight average molecular weight above approximately 3500, the α-olefin has 8 to 12 carbon atoms, and wherein the esterifying component is iso-Cβ alcohol. 12. A copolymer of an α-olefin and a fumaric diester having an aliphatic alcohol as the esterifying component, characterized in that the copolymer has a weight average molecular weight above approximately 3500, the α-olefin has 14 to 16 carbon atoms, and wherein the esterifying component is n-Cg alcohol.

Inventors: MACHEREY HERIBERT JOSEF, WALLFAHRER UWE HANS, MACHEREY, HERIBERT, JOSEF, WALLFAHRER, UWE, HANS
Applicants: AKZO NOBEL NV, MACHEREY HERIBERT JOSEF, WALLFAHRER UWE HANS, AKZO NOBEL N.V., MACHEREY, HERIBERT, JOSEF, WALLFAHRER, UWE, HANS
Application year: 1994
Main classification: C10M107
IPC codes: C08F10, C08F210, C08F222, C08L23, C08L33, C08L35, C10M107, C10M145, C10M169, C10N20, C10N30